A spiral concentrator has a spiral trough (2.001) has a concentrate gutter (2.010) and a pocket (2.008) located near the outer edge of the gutter. An inflatable bladder (2.012) is located in the pocket and can be deformed from a first state in which the bladder does not interfere with the flow of the slurry, to a second state, in which the bladder diverts the concentrate towards a concentrate gutter (2.101). Alternatively, a spiral trough has a deformable device that sits above and separate from the trough and acts as a flow diverter. As the device changes form, shape or state, it gradually contacts the trough or flow diverting more or less concentrate in a controlled manner.
|
1. A spiral concentrator having a spiral trough having an inner rim and an outer rim defining a flow path, including an adjustable flow diverter proximate the flow path, and adapted to adjustably divert at least part of the flow of a slurry in the trough, wherein the adjustable flow diverter includes a deformable member.
2. A spiral concentrator as claimed in
3. A spiral concentrator as claimed in
4. A spiral concentrator as claimed in
5. A spiral concentrator as claimed in
7. A spiral concentrator as claimed in
8. A spiral concentrator as claimed in
9. A spiral concentrator as claimed in
10. A spiral concentrator as claimed in
11. A spiral concentrator as claimed in
12. A spiral concentrator as claimed in
13. A spiral concentrator as claimed in
14. A spiral concentrator as claimed in
|
This invention relates to a spiral concentrator.
Spiral concentrators are used to separate minerals by providing a descending spiral trough down which a mineral slurry flows. The slurry flow is subjected to centrifugal and gravitational forces. The heavier minerals (high density particles) accumulate towards the inner part of the trough and the gangue (low density particles) tend towards the outer part of the trough.
Various modifications to the trough have been proposed to improve yield. An example of a spiral concentrator with a flow diverter can be found in WO02092232.
According to an embodiment of the invention, there is provided a spiral concentrator having a spiral trough having an inner rim and an outer rim, including an adjustable flow diverter proximate the flow path, the flow diverter being adapted to adjustably divert at least part of the flow of a slurry in the trough.
The flow diverter can be controllable.
The adjustable flow diverter can be provided in the floor of the trough.
The adjustable flow diverter can be provided above the floor of the trough.
The adjustable flow diverter can be located proximate the inner rim of the trough.
The adjustable flow diverter can be located between the inner rim of the trough and the outer rim of the trough.
The flow diverter can include a depression in the floor of the trough.
The flow diverter can include a deformable member.
The deformable member can include a bladder.
The bladder can have at least a normal state and a deflated or evacuated state.
The bladder can have a normal state, an inflated state, and a deflated or evacuated state.
A protective layer can be applied to the surface of the bladder
The spiral concentrator can include two or more flow diverters as claimed in any one of the preceding claims.
The flow diverter can be an adjustable piston.
The invention also provides a spiral concentrator having a concentrate gutter.
The flow diverter can be adapted to divert slurry concentrate into the gutter.
The flow diverter can be a device that sits above the surface of the trough and, as it changes physical states, makes contact with the trough to divert flow and, in another state, has no contact with the trough leaving the flow to follow its normal trajectory.
The flow diverter can change form or shape gradually, in order to gradually divert more or less flow as desired.
The flow diverter or deflector can be separate from and proximate the floor of the trough, and can be adapted to contact the flow or the trough or both in a gradual and controlled manner.
Using the diverter, a tailing stream or middling stream can be diverted as desired by an operator.
Controlled deformation of the trough can impose a desired influence on the flow such as improving separation efficiency or altering slurry density or velocity.
Controlled deformation of a device, physically separated from the trough, can be used to impose a desired influence on the flow such as improving separation efficiency or altering slurry density or velocity.
The invention also provides a method of operating a spiral concentrator including the step of adjusting the shape of the flow diverter to discharge concentrate into a concentrate gutter.
An embodiment or embodiments of the present invention will now be described, by way of example only, with reference to the accompanying drawings, in which:
The numbering convention used in the drawings is that the digits in front of the full stop indicate the drawing number, and the digits after the full stop are the element reference numbers. Where possible, the same element reference number is used in different drawings to indicate corresponding elements.
The invention will be described with reference to the embodiments illustrated in the accompanying drawings.
The spiral trough can be connected to the support pipe via a flange 1.015 and suitable fastening means such as bolts, rivets, or welds (not shown). One or more apertures (not shown) in fluid communication with the concentrate channel 1.010 can be provided in the pipe 1.011 through which the concentrate can be diverted from the duct. The pipe can include an inner pipe and an outer pipe, one of the pipes being used to supply slurry or to recycle part of the discharged slurry and the other pipe being used to collect the slurry concentrate.
In operation, the differences in density, between particles of different mineral species, cause them to separate in the slurry as they flow down the trough. The slurry at the inner portion of the trough experiences a steeper angle of descent than the slurry at the outer rim of the trough because both descend the same vertical distance per revolution, but the horizontal distance travelled at the outer rim is greater than at the inner portion of the trough. The concentrate runs off into the concentrate gutter.
Multiple spiral troughs can be wound in parallel around a common axis to increase the throughput.
In the remaining figures, the attachment flange, 1.015 in
The trough of
In a further modification, an adjustable element can be provided to alter the flow of the slurry.
While the pocket and bladder are shown as extending only a short spiral “circumferential” distance near the inner rim, the pocket and bladder can extend for a greater circumferential distance, extending up to the entire length of the trough or a shorter distance depending on the required application. In addition, one or more discrete pockets and bladders can be placed at intervals, or several contiguous bladders can be provided in a single pocket.
In a further embodiment, the adjustable member can extend across the width of the trough to provide repulping or to retard slurry flow.
As shown in
Two or more bladders can be contiguously co-located in a continuous pocket. The upper bladder can be designed to be inflated above the level of the floor of the trough by the use of compressed air or other suitable pressurized fluid. This may be used where it is desired to retain the concentrate in the trough for a specified distance. A second bladder can then be provided contiguously located in relation to the upper bladder, to divert the concentrate at a desired location. The use of several such bladders makes the equipment adaptable for differing slurries, etc.
The bladder can be made of any suitable flexible air tight material which is capable of withstanding the environment of a spiral concentrator. Natural rubber, silicone rubber or polyurethane can be used for the bladder. The bladder can be provided at least on the surfaces exposed to the slurry with an exterior layer or coating to provide added strength and wear resistance. A polyethylene film or any other suitable material can be used for the exterior layer. The exterior layer can be a woven material.
A pneumatically deformable member could also constitute a bellows or telescopic type of device that expands and contracts and need not be formed from highly elastic material such as rubber. The diverter can be formed of separate parts, such as a flexible bladder having a wear-resistant surface in contact with the slurry.
The spiral trough can be made from a resilient material or can have a top layer of resilient material, and a pocket 9.042 can be formed in the base at a desired location. The top surface 9.040 of the pocket can be sufficiently thin to deform in response to pneumatic pressure changes so it can be inflated or deflated as required. Similarly, a side wall of the pocket 9.044 can be sufficiently flexible to permit it to deform under pneumatic pressure changes.
The embodiments described above enable remote manipulation of the shape of the diverter member and hence the ability to influence the operation of the concentrator remotely. Two or more such diverters can be operated simultaneously.
In this specification, reference to a document, disclosure, or other publication or use is not an admission that the document, disclosure, publication or use forms part of the common general knowledge of the skilled worker in the field of this invention at the priority date of this specification, unless otherwise stated.
In this specification, terms indicating orientation or direction, such as “up”, “down”, “vertical”, “horizontal”, “left”, “right” “upright”, “transverse” etc. are not intended to be absolute terms unless the context requires or indicates otherwise.
Where ever it is used, the word “comprising” is to be understood in its “open” sense, that is, in the sense of “including”, and thus not limited to its “closed” sense, that is the sense of “consisting only of”. A corresponding meaning is to be attributed to the corresponding words “comprise”, “comprised” and “comprises” where they appear.
It will be understood that the invention disclosed and defined herein extends to all alternative combinations of two or more of the individual features mentioned or evident from the text. All of these different combinations constitute various alternative aspects of the invention.
While particular embodiments of this invention have been described, it will be evident to those skilled in the art that the present invention may be embodied in other specific forms without departing from the essential characteristics thereof. The present embodiments and examples are therefore to be considered in all respects as illustrative and not restrictive, and all modifications which would be obvious to those skilled in the art are therefore intended to be embraced therein.
Patent | Priority | Assignee | Title |
Patent | Priority | Assignee | Title |
4597861, | Apr 13 1983 | Clyde Industries Limited | Spiral separator |
4747943, | Nov 30 1984 | Clyde Industries Limited | Splitter assembly |
4819720, | Nov 09 1984 | McDonnell Douglas Corporation | Skin heat exchanger |
5452805, | Feb 02 1994 | Carpco, Inc. | Spiral separator |
6264041, | Jan 26 2000 | Outokumpu Oyj | Adjustable splitter assembly for spiral separator |
6336559, | Nov 24 1999 | OUTOKUMPU OYJ, | Spiral separator with replaceable trough sections |
7686170, | May 17 2002 | Mineral Technologies Pty Ltd | Deflector for spiral separator, and method of spiral separation |
EP149518, | |||
EP2123361, | |||
GB586777, | |||
SU1260024, | |||
WO2005107963, |
Executed on | Assignor | Assignee | Conveyance | Frame | Reel | Doc |
Jul 30 2009 | CPG Resources-Mineral Technologies Pty Ltd | (assignment on the face of the patent) | / | |||
Mar 02 2011 | COOKE, GRAEME | CPG Resources-Mineral Technologies Pty Ltd | ASSIGNMENT OF ASSIGNORS INTEREST SEE DOCUMENT FOR DETAILS | 025906 | /0938 |
Date | Maintenance Fee Events |
Oct 13 2016 | M1551: Payment of Maintenance Fee, 4th Year, Large Entity. |
Nov 30 2020 | M1552: Payment of Maintenance Fee, 8th Year, Large Entity. |
Date | Maintenance Schedule |
Jun 11 2016 | 4 years fee payment window open |
Dec 11 2016 | 6 months grace period start (w surcharge) |
Jun 11 2017 | patent expiry (for year 4) |
Jun 11 2019 | 2 years to revive unintentionally abandoned end. (for year 4) |
Jun 11 2020 | 8 years fee payment window open |
Dec 11 2020 | 6 months grace period start (w surcharge) |
Jun 11 2021 | patent expiry (for year 8) |
Jun 11 2023 | 2 years to revive unintentionally abandoned end. (for year 8) |
Jun 11 2024 | 12 years fee payment window open |
Dec 11 2024 | 6 months grace period start (w surcharge) |
Jun 11 2025 | patent expiry (for year 12) |
Jun 11 2027 | 2 years to revive unintentionally abandoned end. (for year 12) |